U.S. patent number 3,916,152 [Application Number 05/523,330] was granted by the patent office on 1975-10-28 for temperature control system for a centrifugal-type chemistry analyzer.
This patent grant is currently assigned to Union Carbide Corporation. Invention is credited to Clyde D. Hinman.
United States Patent |
3,916,152 |
Hinman |
October 28, 1975 |
Temperature control system for a centrifugal-type chemistry
analyzer
Abstract
A temperature control system for raising and controlling the
temperature of small volumes of liquid by heating the liquid and
detecting the instantaneous temperature and rate of temperature
increase and utilizing this information to control the heating of
the liquid so that the desired liquid temperature is attained and
maintained in a minimum time interval.
Inventors: |
Hinman; Clyde D. (Wilton,
CT) |
Assignee: |
Union Carbide Corporation (New
York, NY)
|
Family
ID: |
26946527 |
Appl.
No.: |
05/523,330 |
Filed: |
November 13, 1974 |
Related U.S. Patent Documents
|
|
|
|
|
|
|
Application
Number |
Filing Date |
Patent Number |
Issue Date |
|
|
258259 |
May 31, 1972 |
3683049 |
|
|
|
Current U.S.
Class: |
219/389; 219/494;
392/379; 494/1; 494/10; 494/13; 165/299 |
Current CPC
Class: |
B01L
7/00 (20130101); G05D 23/1909 (20130101); G05D
23/24 (20130101) |
Current International
Class: |
B01L
7/00 (20060101); G05D 23/20 (20060101); G05D
23/24 (20060101); G05D 23/19 (20060101); F27B
007/00 (); F27D 011/02 () |
Field of
Search: |
;219/370,385,388,389,400,413,430,441,494 ;165/39 ;34/8,58,59
;233/11 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Mayewsky; Volodymyr Y.
Attorney, Agent or Firm: McCarthy; F. J.
Parent Case Text
This is a division of application Ser. No. 258,259 filed May 31,
1972, now U.S. Pat. No. 3,863,049.
Claims
We claim:
1. A system for controlling the temperature of a reaction chamber
adapted to containing liquid comprising, in combination, heating
means adapted to develop heat by the passage of electrical current
therethrough, means for transferring heat developed in the heating
means to the reaction chamber to raise the temperature thereof to a
desired value, temperature sensing means adapted to provide an
electrical signal proportional to the amount by which the reaction
chamber temperature is below the desired value, control means
responsive to the signal of the temperature sensing means adapted
to supply electrical energy to the heating element, rate detecting
means for obtaining an electrical signal proportional to the rate
of temperature increase of the reaction chamber and for applying
such electrical signal to the control means to inactivate the
control means when the rate of temperature increase is above a
predetermined value, means for preventing the signal from the rate
detecting means from inactivating the control means as long as the
reaction chamber temperature is below a pre-determined value.
2. A system in accordance with claim 1 wherein the reaction chamber
is substantially separated from ambient temperatures by an
enclosing housing member and means are provided to pass air in
contact with the heating means and then into the housing member to
transfer heat developed in the heating means to the reaction
chamber.
3. A system in accordance with claim 1 wherein means are provided
for supporting the reaction chamber, said means being in heat
transfer relationship with the reaction chamber and having a
substantially higher thermal mass than any liquid contained in the
reaction chamber and being adapted to be heated to the desired
reaction chamber temperature.
Description
The present invention is directed to an improved temperature
control system. More particularly, the present invention is
directed to a temperature control system for controlling the
temperature of small volumes of liquid undergoing analysis in a
centrifugal-type chemistry analyzer.
Centrifugal-type chemistry analyzers, such as the type disclosed in
"Analytical Biochemistry," 28 545-562 (1969) introduce by
centrifugal force small volumes of liquid sample and reagent, e.g.,
a combined volume of 300-600 milliliters into a series of cuvettes
arranged around the periphery of a rotor. The reaction in the
curvettes is monitored with precision by photometric means. The
reactions involved are usually temperature sensitive, with a
constant temperature in the range of 25.degree. to 40.degree. being
usually required. Since the liquids involved in the tests are
rarely at the desired temperature to begin with, and often are
under refrigeration until just prior to testing, it is important
that a system is provided for raising and controlling the
temperature of the liquids involved. Also, since most of the
reactions involved in the use of centrifugal analyzers proceed
rapidly, it is important that the temperature of the test liquid be
brought rapidly, e.g., within about 30 to 40 seconds, to the
desired value and held closely at this value throughout the testing
period.
It is therefore an object of the present invention to provide a
system for raising and accurately controlling the temperature of
small volumes of test liquids in a centrifugal-type chemistry
analyzer.
Other objects will be apparent from the following description and
claims taken in conjunction with the drawing wherein
FIG. 1 is a sectional elevation view of a centrifugal type
analyzer,
FIG. 2 is a plan view of the analyzer of FIG. 1 showing means for
applying heated air to the analyzer,
FIG. 3 shows a series of curves representing various heating
conditions in an analyzer of the type illustrated in FIG. 1,
FIG. 4 shows a block diagram of the temperature control system of
the present invention, and
FIG. 5 shows a specific embodiment of a temperature control system
in accordance with the present invention.
With reference to the drawing FIG. 1 shows in elevation a
centrifugal-type analyzer comprising a removable sample-reagent
disc 10 supported on a rotor 11 and indexed thereto by pin 14.
Rotor 11 is affixed to drive assembly 12 by pin 15. Drive assembly
12 is rotatably driven by way of V-belt pulley 13 attached to drive
shaft 17. The portion 16 of rotor 11 is suitably of stainless steel
over which is arranged a glass plate 18. The body portion 20 of
sample-reagent disc 10 is suitably formed of Teflon (Trademark of
E. I. duPont de Nemours) and contains a plurality, usually about
30, of concentrically arranged inter-connecting cavities indicated
at 22. Reagent cavity 24, contains for example a glucose reagent
such as a 0.3 molar triethanolamine buffer of pH 7.5 containing
0.0004 Mol/liter NADP, 0.0005 Mol/liter ATP, 70 mg/liter
hexokinase, 140 mg/liter glucose-6-phosphate dehydrogenase and
0.004 Mol/liter MgSO.sub.4. The reagent, indicated at 26, upon
spinning of the sample-reagent disc 10, passes into sample cavity
28, containing for example blood serum, and both liquids pass via
transfer passage 30 into cuvette 32 located in ring member 34 which
is affixed at 31 to rotor 11. Cuvette 32, and all other cuvettes,
are enclosed by ring member 34 and are in heat transfer relation
therewith. Ring member 34 is formed of aluminum, coated for
corrosion resistance purposes with a thin layer of Teflon 35 in
which is mounted a temperature sensing element, e.g., a thermistor,
indicated at 36 which is adapted to provide an electrical signal
indication of the temperature of the liquid in cuvette 32. Cuvettes
32 are also provided with a thin Teflon coating 33 for purposes of
corrosion resistance. The extent of the reaction between the
liquids in cuvette 32 is measured photometrically by means of light
source 38 and photomultiplier 40. The electrical signal derived
from thermistor 36 is conducted via wire leads 41 to slip rings 42
and to brushes 44 from which the signal is conducted by wires 46 to
the temperature controlling circuit illustrated in FIGS. 4 and 5
hereinafter more fully described.
As shown in FIG. 1, the reaction in the cuvettes will take place
within a substantially confined space enclosed by metal housing 48,
plastic ring shield member 50 and plastic cap member 52. This
arrangement essentially separates the interior of the housing from
the outside ambient temperature conditions. Hot air, controlled by
the circuit of FIGS. 4 and 5 is introduced into the confined
reaction environment at opening 54 and exits through openings 56 in
housing 48. The general heating arrangement is illustrated in FIG.
2 which shows schematically a conventional blower motor and blower
unit 60 which forces air over heating element 62 through duct 64
and into housing 48.
With reference to FIG. 3 of the drawing, this Figure shows a series
of curves, obtainable using a conventional "Brush" millivolt
recorder which relate to the raising of the temperature of a liquid
in a cuvette 32 to a desired temperature. Curve A represents the
characteristic variation of temperature with time in the cuvette
upon introduction of cold liquid into the cuvette without any heat
being added. This characteristic variation is obtained in the
practice of the present invention due to the fact that the cuvette
is located in a member, i.e., aluminum ring member 34, which has a
substantially larger thermal mass than the liquid in the cuvette
and is at the desired reaction temperature. Ring member 34 can be
quickly raised to the desired reaction temperature simply by
actuating the control circuit without any liquid in the cuvettes.
The heat stroed in the ring member is conducted to the liquid in
the cuvettes causing the cuvette temperature to rise as generally
indicated by curve (A). The temperature control system of the
present invention is most effective, if the temperature of the
liquid in the cuvettes be raised, without the direct application of
heat, from an initial "cold" condition in the range of about
15.degree. to 20.degree.C, to witnin 0.4.degree. to 0.8.degree.C of
the desired value in the range of about 25.degree. to 40.degree.C,
within 20 to 40 seconds. This can be readily provided through the
use of a metal ring member 34 having a thermal mass of about 5 to
20 times or more of the thermal mass of the total liquid in the
cuvettes. Aluminum is preferred for the ring member 34 because of
its high heat conductivity although generally all structural metals
and high heat conducting materials can be used. By way of example,
the thermal mass of a 1 kilogram aluminum ring member would be 1000
.times. 0.23 (the specific heat of aluminum) or about 230. The
thermal mass of 12 grams of reagent plus sample (95% or more water)
would be 12 .times. 1 (the specific heat of water) or about 12. The
ratio of the thermal mass of the ring to the liquid would be about
20. A ring member of about 2500 grams of copper would provide about
the same ratio. Care should be taken in coating the cuvette with
any substance that introduces significant thermal resistance
between the liquid in the cuvette and the ring member so that the
desired temperature increase is not unduly delayed. For example, a
3-7 mil Teflon coating has been found to be satisfactory where a
ring to liquid thermal mass ratio of about 20 is provided.
Referring further to FIG. 3, at time T.sub.1 the temperature in the
empty cuvette is the desired value, e.g., 30.degree.C. The
temperature in the cuvette is initially at the desired value, e.g.,
30.degree.C, due to prior heating of ring member 34 with hot air
from the heater unit illustrated in FIG. 2. When cold liquid fills
the cuvette the temperature drops rapidly and then, on account of
the heat stored in the relatively large rotor mass, and the small
liquid volume in the cuvette, the temperature fairly rapidly rises.
However the temperature in the cuvette will never get within a
tolerable value of the desired temperature, e.g. .+-.0.1.degree.C,
indicated at 100 without the addition of heat.
If excess heat is rapidly and continuously applied to the enclosed
cuvette system from time T.sub.1 to T.sub.2, the temperature-time
relationship will be generally as indicated in curve "B", i.e., the
desired temperature will be reached rapidly and then exceeded by an
undesirably large amount and will "over shoot" requiring a
relatively long time to return to within an acceptable tolerance of
the desired value as indicated at T.sub.3. If, on the other hand,
insufficient heat is applied, the situation approaches the
condition of curve "A."
The desirable situation is illustrated by curve "C" when the
temperature rapidly reaches the desired value and where any "over
shoot" is within the acceptable tolerance, e.g., about
0.1.degree.C.
This is accomplished in the present invention by the arrangement
illustrated in FIGS. 4 and 5. With reference to FIG. 4, the output
voltage signal from the cuvette thermistor 36 is applied to a
standard bridge circuit 100 having adjustments 101, 103 and 105
whereby the bridge circuit 100 will indicate a "zero" value when
the signal from thermistor 36 corresponds to the pre-set desired
temperature, e.g., 30.degree.C. In the case where a cold sample is
introduced into the cuvette, the signal from thermistor 36 will
cause the bridge 100 to be unbalanced and a signal proportional to
the temperature difference, indicated at 135, will be applied to
amplifier 110 to actuate trigger unit 120. Pulses from the trigger
unit 120 are applied to a power switch 130 which permits
alternating current power to be applied to how air heater 140 so
long as pulses are received from trigger unit 120. The hot air from
heater 140 is directed to the cuvette rotor assembly as previously
described to raise the temperature in the cuvette. When the "no
added heat" profile (curve A) of the unit is approximately known as
shown in FIG. 3, an initial "hold off" temperature can be
estimated. This "hold off" temperature can be initially selected as
about one-half the total temperature drop, indicated at 145 in FIG.
3. This "hold off" may be on the order of 2.degree.C. With the
approximate "hold off" value determined, "hold off" circuit 150 is
set so that the output of rate limiter circuit 160 is isolated from
the trigger circuit 120 by gate 165 for as long as the temperature
in the cuvette is below the set "hold off" temperature. Under these
circumstances, the signal from bridge 100 is applied via amplifier
110 to trigger circuit 120 and heater 140 supplies heat to the
cuvette containing ring member 34. When the temperature in the
cuvette raises to the "hold off" level, the output of rate limiter
circuit 160 will be applied to trigger circuit 120 by the closing
of "hold off" gate 165. Rate limiter circuit 160 detects the
increase in rate of the output of amplifier 110, i.e., the rate of
temperature increase in the cuvette. If the rate of temperature
increase is too fast, as compared to a predetermined value, i.e.,
an "over shoot" will eventually occur unless heating is
discontinued, and under these conditions, a signal from the rate
limiter circuit 160 "turn off" the trigger circuit 120. Heat is no
longer applied to the rotor assembly until the rate of temperature
increase falls below the desired predetermined value, at which time
the signal of rate limter 160 is no longer applied to trigger
circuit 120 and heat is again supplied to the rotor assembly. This
operation continues until the desired temperature is reached and
"zero" output is present at bridge 100. The desired pre-selected
rate of temperature increase to provide a temperature profile as
indicated at "C" can be obtained by trial and error. Also, this
rate can be initially approximated by obtaining a "no heat added"
profile, such as curve (A) and marking off an increment equal to
the maximum permissable temperature tolerance, e.g., 0.1.degree.C,
as indicated at 115. The corresponding slope on curve (A),
indicated at 167, can serve as a first approximation of the maximum
desired rate. Further routine adjustment of the rate limiter
circuit will optimize the heating cycle. In the event that with the
initial "hold off" setting, the rate limiter circuit 160 never
"turns on," i.e., the maximum desired slope is always exceeded,
then lower "hold off" settings should be successively applied until
the rate limiter circuit 160 becomes operative. The maximum rate
setting can then be adjusted to minimize the time T.sub.4 required
to reach an acceptable temperature. For most tests using a
centrifugal photometric analyzer, this time should be less than 30
to 40 seconds.
With further reference to curve C of FIG. 3, illustrating a
temperature curve where temperature control is provided in
accordance with the present invention, continuous hot air is
supplied in the interval T.sub.1 to T.sub.1 '. Hot air is then
turned off until the slope of curve C decreases at 490 to just
below the maximum desired slope 500. Rate Limiter circuit 160 then
causes hot air to be re-applied and the maximum desired rate of
temperature increase is essentially maintained until the desired
temperature is achieved at 510, at which time the control system of
"off" since the voltage at the output of bridge 100 is "zero." The
cuvette temperature will then "over shoot" only within the desired
tolerance. In the event that curve C goes below the desired
tolerance at 520 a signal will be developed at bridge 100 and
trigger circuit 120 will cause heat to be re-applied and the
temperature will be maintained within the desired tolerance.
FIG. 5 illustrates more specifically the system of FIG. 4. With
reference to FIG. 5 the output of cuvette thermistor 36 is applied
via slip rings 42 to bridge circuit 100 which, in addition to
thermistor 36, comprises fixed resistors 300 and 302 and the
conventional adjustable resistor arrangement which includes fixed
resistors 306, 308 and 310 and adjustable resitors 312, 314 and
316. Switch 318 is positioned to select the temperature value at
which the bridge output will be "zero," i.e., balanced, for the
desired cuvette temperature. For example, if the desired cuvette
temperature is to be 30.degree.C, switch 318 is placed in that
position and a temperature of 30.degree.C established in the
cuvette. Adjustable resistor 314 is then varied until the bridge
output at 320, more practically, the amplifier output at 340, is
"zero." The bridge circuit 100 is thus calibrated for a desired
cuvette temperature of 30.degree.C. The bridge can be similarly
calibrated for other desired cuvette temperatures. The output of
bridge circuit 100 is applied to amplifier 110, for example a
commercial differential amplifier such as Fairchild .mu. A 725.
Customary +15 VDC and -15VDC supplies to amplifier 110 are provided
at 322 and 324 respectively. A conventional feedback circuit 326,
comprising resistor 328 and capacitor 330, is provided together
with a conventional temperature balancing resistor 334. The output
of amplifier 110 appears at resistor 338. By way of example, if the
output of bridge circiut 100 is 0.02 volts for each degree
centigrade that the cuvette temperature is below the desired
temperature (which can be determined by routine calibration)
amplifier 110 will provide an increased signal, e.g., 1 volts per
degree centigrade, depending on the amplifier gain. Under these
exemplary circumstances, if upon introduction of cold test liquid
into the cuvette, the temperature drops from its initial value of
30.degree. to 20.degree.C, an output signal of 10 volts will be
provided at location 340 at the output of amplifier 110. This
signal is applied at the input 342 of trigger circuit 120 and the
input 344 of "hold off" circuit 150. As shown in FIG. 5. "hold off"
circuit 150 comprises amplifier 344, which can be a commercial
differential amplifier such as Fairchild .mu. A741, which is
provided with +15 volts and -15 volts at 346 and 348. A reference
voltage input signal for "hold off" amplifier 344 is provided by
way of adjustable resistor 350 and fixed resistor 352 supplied with
+15VDC as indicated at 354. This reference signal from adjustable
resistor 350 is the "hold off" signal. For example, if as
previously noted, the desired cuvette temperature is 30.degree.C,
and the cuvette temperature falls to 20.degree.C upon introduction
of cold test liquid, the "hold off" voltage at adjustable resistor
350 can be set to 5 volts as a first approximation, if the output
of amplifier 110 is 1 volt per degree centigrade, as previously
given by way of example. Under these circumstances, as long as the
output of bridge amplifier 110 is more than 5 volts, a signal is
provided at the output of "hold off" amplifier 344 which, due to
gate arrangement 165 (comprising diodes 353 and 355), prevents an
inhibiting signal from passing from rate limiter circuit 160 to
trigger circuit 120. Consequently, the signal from bridge amplifier
110 is applied to trigger circuit 120 at 342, and causes electrical
pulses to be applied to power switch 130 whereupon AC power is
passed through heater element 62 of air heater 140 and hot air is
delivered to the enclosure surrounding the cuvette as previously
described, whereby the cuvette temperature is increased. Trigger
circuit 120 can be a commercial unit such as Fairchild .mu. A 742
and is arranged to receive an AC reference signal at 356 by way of
transformer 359, and DC power at 358 through the arrangement
comprising resistors 360 and 362, diode 364 and filter circuit 366.
With a positive signal applied to the trigger circuit 120 at 342,
output pulses appear at 367 and are applied via transformer 370 and
power switch 130 to heater element 62 until an inhibiting signal,
e.g., 15 volts DC is applied at 368.
Such an inhibiting signal will be applied when the output of bridge
amplifier 110 increases greater than the pre-set rate of voltage
increase due to the heating of the cuvette by hot air supplied from
air heater 140. At this time, gate 165 will "open," permitting the
signal at the output 370 (if a signal is present) to be applied at
the input 368 of trigger circuit 120 which "turns off" the trigger
circuit 120 discontinuing the application of hot air to the
cuvette. Whether an inhibiting signal is present at the output 370
of the rate limiter circuit 160 depends on the rate of increase of
the output signal of bridge amplifier 110 (which is proportional to
the rate of temperature rise in the cuvette) and the desired
maximum rate of cuvette temperature increase, determined for
example in the manner previously described in connection with FIG.
3. The rate of increase for the output signal of bridge amplifier
110 is detected by a conventional derivative circuit 372 comprising
capacitor 374 and resistor 376. The derivative, or rate signal
obtained is applied at 378 to amplifier 380, which can be a
commercial differential amplifier such as Fairchild .mu.A741.
Amplifier 380 also receives a reference signal at 382 from
temperature compensating resistor 382, which corresponds to the
desired maximum rate and is set by adjustment of variable resistor
384. For example, if the maximum desired rate of temperature
increase is 0.01.degree.C/second, the pre-set voltage at 382 would,
neglecting off-set in amplifier 380, be 0.88 millivolts for a
typical value of 22K ohms for resistor 376 and 4 microfarads for
capacitor 374. Any off-set in amplifier 380 can be taken care of by
adjustment of variable resistor 384. For as long as the voltage at
378 is larger in magnitude (more negative) than this value (0.88
mv) i.e., the rate of temperature increase is above the desired
maximum, the output of amplifier 380 is a positive signal, e.g.,
+15VDC, and an inhibiting signal is applied via gate 165 to trigger
circuit 120 and heater unit 140 will be inactive. When, however,
the voltage at 378 is lower than the pre-set value (0.88 mv) i.e.,
the rate of temperature increase is below the desired pre-set
value, the output of amplifier 380 becomes negative and this signal
is blocked by diode 355 whereupon trigger circuit 120, and hence
heater unit 140, is activated to supply additional hot air to the
cuvette and raise the temperature at a faster rate. This procedure
then continues until the desired cuvette temperature is reached,
e.g., 30.degree.C, at which time the output of bridge amplifier 110
is "zero" and circuit operation ceases.
If it is desired for further reduce the time required to reach the
desired cuvette temperature, the pre-set rate voltage at 382 can be
gradually increased while avoiding an undesirable temperature "over
shoot. "
In the event that, with the initial estimated pre-set "hold off"
voltage, the inhibiting signal of the rate limiter amplifier 380 is
never applied to trigger circuit 120, i.e., the rate limiter never
"cuts in," the likelihood is that the "hold off" signal at 350, at
the input to amplifier, is too small in magnitude and should be
gradually increased in magnitude until the rate limiter 160 "cuts
in" at least once before the desired temperature is reached.
By way of example, in the operation of a particular embodiment of
the present invention the cuvette containing ring member
(containing 30 cuvettes having a volume 0.45 to 0.6 milliliters
each) was formed of an aluminum ring (cross section of
approximately 1 3/8 inches .times. 7/8 inches) having an inner
diameter of 5 1/2 inches and an outer diameter of 8 1/4inches. The
weight of the ring member was about 1 kilogram and the effective
heat transfer area was 30-35 in.sup.2. The outer surfaces of the
aluminum ring member, and also the inner cuvette surfaces, were
coated with a layer of Teflon about 3-9 mils thick. The aluminum
ring member was located in an aluminum housing similar to the
arrangement shown in FIG. 1. The outer diameter of the housing
formed of 1/8 -inch aluminum was approximately 10 inches and the
height was about 6-7 inches. The housing was affixed to a base
plate of 1/2 inch thick aluminum. The top of the housing was
essentially closed by plastic members made of polystyrene. The ring
member and sample-reagent disc were rotated at 1000 RPM and the 30
cuvettes were each filled with about 0.4 milliliters of sample and
reagent at a temperature of 15.degree. to 20.degree.C so that a
total of about 12 grams of liquid was introduced into the cuvette
containing ring member. Since the liquid was 95% or more H.sub.2 O,
this is the thermal equivalent of about 12 grams of water. The
aluminum cuvette containing ring member was intially at a
temperature of 30.degree.C, due to previous heating, which was the
desired cuvette reaction temperature. Heated air was available,
through a duct arrangement as indicated in FIG. 1, at about
65.degree.C and 20 cubic feet per minute from a heater unit
controlled by the system of the present invention. The desired
reaction temperature of 30.degree. C was reached within about 30
seconds and maintained within .+-.0.1.degree.C by the action of the
control system of the present invention.
The temperature control system of the present invention has a high
degree of flexibility. For example, with the system adjusted to
provide a cuvette temperature control as indicated in curve (C) in
FIG. 3, for the largest and closest liquid sample to be handled by
the centrifugal analyzer, smaller and less cold samples will be
raised to the desired temperature (and maintained at this
temperature) within the required time without any need for further
adjustment of the system. Such smaller and less cold samples are
indicated as curves D and E in FIG. 3. For curve D, heated air will
be intially continuously supplied for only the relatively short
interval (d) after which heat control is provided by operation of
the rate limiter circuit 160 in the manner previously described.
For curve E, initial continuous heating will not be provided and
heat control will be provided only by operation of rate limiter
circuit 160. Of course, if desired, optimization of time required
to raise the D- and E-type samples to the desired temperature can
be achieved following the procedure previously described.
* * * * *